EP0657478A2 - Procédé de préparation de dispersion de polymères solubles dans l'eau - Google Patents
Procédé de préparation de dispersion de polymères solubles dans l'eau Download PDFInfo
- Publication number
- EP0657478A2 EP0657478A2 EP94119536A EP94119536A EP0657478A2 EP 0657478 A2 EP0657478 A2 EP 0657478A2 EP 94119536 A EP94119536 A EP 94119536A EP 94119536 A EP94119536 A EP 94119536A EP 0657478 A2 EP0657478 A2 EP 0657478A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- meth
- carbon atoms
- group
- general formula
- acrylamide
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
- WTDPKNJVPQPMKF-UHFFFAOYSA-N CC1=CCC2C1C2 Chemical compound CC1=CCC2C1C2 WTDPKNJVPQPMKF-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F220/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
- C08F220/02—Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
- C08F220/10—Esters
- C08F220/34—Esters containing nitrogen, e.g. N,N-dimethylaminoethyl (meth)acrylate
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F220/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
- C08F220/02—Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
- C08F220/52—Amides or imides
- C08F220/54—Amides, e.g. N,N-dimethylacrylamide or N-isopropylacrylamide
- C08F220/60—Amides, e.g. N,N-dimethylacrylamide or N-isopropylacrylamide containing nitrogen in addition to the carbonamido nitrogen
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F220/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
- C08F220/02—Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
- C08F220/10—Esters
- C08F220/34—Esters containing nitrogen, e.g. N,N-dimethylaminoethyl (meth)acrylate
- C08F220/36—Esters containing nitrogen, e.g. N,N-dimethylaminoethyl (meth)acrylate containing oxygen in addition to the carboxy oxygen, e.g. 2-N-morpholinoethyl (meth)acrylate or 2-isocyanatoethyl (meth)acrylate
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F220/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
- C08F220/02—Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
- C08F220/52—Amides or imides
- C08F220/54—Amides, e.g. N,N-dimethylacrylamide or N-isopropylacrylamide
- C08F220/60—Amides, e.g. N,N-dimethylacrylamide or N-isopropylacrylamide containing nitrogen in addition to the carbonamido nitrogen
- C08F220/603—Amides, e.g. N,N-dimethylacrylamide or N-isopropylacrylamide containing nitrogen in addition to the carbonamido nitrogen and containing oxygen in addition to the carbonamido oxygen and nitrogen
Definitions
- the present invention relates to the novel process for the production of a dispersion of a water soluble polymer.
- This process for the production of a water soluble dispersion includes the polymerization of water soluble monomers of 5 to 100 mole % of a cationic monomer represented by the following formula (I), 0 to 50 mole % of another cationic monomer represented by the following formula (II) and 0 to 95 mole % (meth)acrylamide in the presence of 1 to 10% by weight of an organic high molecular multivalent cation comprising a water soluble polymer containing at least a monomer of formula (II) (i.e., a hydrophilic monomer), based on the total weight of the monomers, in an aqueous multivalent anionic salt solution having a concentration of 15% by weight or more: where R1 is either hydrogen or CH3; R2 and R3 are each an alkyl group having 1 to 3 carbon atoms; A1 is either an oxygen atom or NH; B1 is either an alkylene group having 2 to 4 carbon atoms or a hydroxypropylene group, and X1
- the water soluble cationic polymer that is insoluble in the aqueous solution of polyvalent anionic salt contains at least 5 mole % of cationic monomer units represented by the aforementioned general formula (I) above and the water soluble cationic polymer that is soluble In the aqueous solution of a polyvalent anionic salt contains at least 20 mole % of cationic monomer units represented by the general formula (II) above.
- the multivalent anionic salt concentration can be optimized to control process viscosity.
- This optimization of the multivalent anionic concentration has been demonstrated to control the particle size as well as facilitate the precipitation process by very significantly reducing the process viscosity.
- This allows the production of high molecular weight polymer dispersions in a low viscosity reactor, thereby avoiding the substantial costs associated with high viscosity custom built polymerization reactors.
- the reduction In process viscosity will allow the preparation of polymer systems containing higher actives (such as, from 15 to about 30 percent by weight or above) in high viscosity latex-type reactors.
- the dispersion is prepared by polymerizing a water soluble mixture of from about 15 to about 30% percent by weight of a cationic monomer represented by the following general formula (I): where R1 is either hydrogen or CH3; R2 and R3 are each an alkyl group having 1 to 3 carbon atoms; A1 is either an oxygen atom or NH; B1 is either an alkylene group having 2 to 4 carbon atoms or a hydroxypropylene group, and X1 ⁇ is an anionic counterion, and/or a second cationic monomer represented by the following general formula (II): where R4 is either hydrogen or CH3; R5 and R6 are each an alkyl group having 1 to 2 carbon atoms; R7 is a hydrogen atom or an alkyl group having 1 to 2 carbon atoms; A2 is either an oxygen atom or NH; B2 is either an alkylene group having
- the present invention is particularly useful in processes for preparing a water soluble polymer dispersion.
- the dispersion is prepared by polymerizing a water soluble mixture of a cationic monomer represented by the following general formula (I): where R1 is either hydrogen or CH3; R2 and R3 are each an alkyl group having 1 to 3 carbon atoms; A1 is either an oxygen atom or NH; B1 is either an alkylene group having 2 to 4 carbon atoms or a hydroxypropylene group, and X1 ⁇ is an anionic counterion, and/or a second cationic monomer represented by the following general formula (II): where R4 is either hydrogen or CH3; R5 and R6 are each an alkyl group having 1 to 2 carbon atoms; R7 is a hydrogen atom or an alkyl group having 1 to 2 carbon atoms; A2 is either an oxygen atom or NH; B2 is either an alkylene group having 2 to 4 carbon atoms or a hydroxypropy
- the (meth)acrylamide is typically present in an amount in the range between about 20 to about 95 mole %, the cationic monomer represented by the general formula (I) is typically present in an amount between about 5 to about 50 mole %; and the cationic monomer represented by the general formula (II) is typically present in an amount between about 5 to about 50 mole %.
- the use of the cationic monomer represented by the general formula (II) is optional.
- the dispersant system of the invention is present in an amount between about 2.5 to about 6 weight %, based on the total weight of the monomers of the dispersion.
- Examples of monomers represented by the general formula (I) include quaternary monomers obtained by treating dimethylaminoethyl (meth)acrylate, diethylaminoethyl (meth)acrylate, dimethylaminopropyl (meth)acrylamide and dimethylhydroxypropyl (meth)acrylate, diethylaminopropyl (meth)acrylamide and dimethylaminohydroxylpropyl (meth)acrylate with benzyl chloride.
- One preferred monomer is N-benzyl-N-(meth)acryloxyethyl-N,N-dimethylammonium chloride.
- Examples of monomers represented by the general formula (II) include salts such as dimethylaminoethyl (meth)acrylate, diethylaminoethyl (meth)acrylate, dimethylaminopropyl (meth)acrylamide, diethylaminopropyl (methyl)acrylamide and dimethylhydroxypropyl (meth)acrylate, and methylated and ethylated quaternary salts.
- One preferred monomer is N-(meth)acryloyloxyethyl-N,N,N-trimethyl ammonium chloride.
- the polymer initiator is selected from the group consisting of 2,2'-azobis(2-amidinopropane) hydrochloride (V50), ammonium persulfate, 2,2'-azobis (N,N'-dimethylene isobutyramidine) dihydrochloride (VA044), and ammonium persulfate/sodium meta bisulfite.
- the inventors have discovered that process viscosities can be carefully controlled by controlling the concentration of the multivalent anionic salt used to deposit the polymer of the present invention.
- the multivalent anionic salt in the present invention is preferably a sulfate or a phosphate, and typical examples of these salts include ammonium sulfate, sodium sulfate, magnesium sulfate, aluminum sulfate, ammonium hydrogenphosphate, sodium hydrogenphosphate and potassium hydrogenphosphate.
- the salt is used in the form an aqueous salt solution at a concentration of from about 17 to about 19 by weight, more preferably 17.0 to about 17.50 percent by weight and most preferably, about 17.20 percent by weight.
- the concentration of the multivalent anionic salt permits the use of conventional latex reactors since the process viscosity during polymerization is maintained below about 25,000 cp, more preferably below about 15,000 cp and most preferably about 5,000 cp.
- the present inventions have determined that an aqueous salt concentration during the polymerization, of more than 19 percent by weight or less than 17 percent by weight produces process viscosities which are too great for low viscosity reactors to handle.
- the monomer mixture, water, ammonium sulfate, benzyl alcohol and versene are added in a batch reactor.
- the contents were heated to 48°C and, thereafter, nitrogen purged.
- Polymerization initiator, V-50 was added to the batch reactor. After the addition, the reactants were held in the reactor for four hours at 48°C.
- the reaction products were cooled to room temperature and post reaction addition of ammonium salt were added to prevent polymer degradation and, optionally, acetic acid and ammonium thiocyanate.
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Polymerisation Methods In General (AREA)
- Colloid Chemistry (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US16377993A | 1993-12-09 | 1993-12-09 | |
US163779 | 1993-12-09 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0657478A2 true EP0657478A2 (fr) | 1995-06-14 |
EP0657478A3 EP0657478A3 (fr) | 1995-07-26 |
Family
ID=22591533
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP94119536A Withdrawn EP0657478A3 (fr) | 1993-12-09 | 1994-12-09 | Procédé de préparation de dispersion de polymères solubles dans l'eau. |
Country Status (6)
Country | Link |
---|---|
EP (1) | EP0657478A3 (fr) |
JP (1) | JPH07238121A (fr) |
KR (1) | KR950018176A (fr) |
AU (1) | AU8024794A (fr) |
BR (1) | BR9404916A (fr) |
CA (1) | CA2137637A1 (fr) |
Cited By (44)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5614602A (en) * | 1996-07-09 | 1997-03-25 | Betzdearborn Inc. | Process for the preparation of aqueous dispersion polymers |
US5696228A (en) * | 1996-10-03 | 1997-12-09 | Cytec Technology Corp. | Process for producing substantially dry polymer particles from aqueous dispersions |
US5733462A (en) * | 1996-10-03 | 1998-03-31 | Cytec Technology Corp. | Cationic water-soluble polymer precipitation in salt solutions |
US5738794A (en) * | 1996-10-03 | 1998-04-14 | Cytec Technology Corp. | Cationic water-soluble polymer preciptation in salt solutions |
US5792366A (en) * | 1996-10-03 | 1998-08-11 | Cytec Technology Corp. | Aqueous dispersions |
US5843320A (en) * | 1996-10-03 | 1998-12-01 | Cytec Technology Corp. | Aqueous dispersions |
FR2770527A1 (fr) * | 1997-11-04 | 1999-05-07 | Atochem Elf Sa | Dispersions aqueuses salines de polymeres hydrosolubles contenant un dispersant amphiphile a base de polymere cationique ayant des motifs hydrophobes |
US5919854A (en) * | 1996-10-03 | 1999-07-06 | Cytec Technology Corp. | Process for preparing aqueous dispersions |
US6013708A (en) * | 1996-10-03 | 2000-01-11 | Cytec Technology Corp. | Cationic water-soluble polymer precipitation in salt solutions |
US6020422A (en) * | 1996-11-15 | 2000-02-01 | Betzdearborn Inc. | Aqueous dispersion polymers |
WO2000011053A1 (fr) * | 1998-08-24 | 2000-03-02 | Green Technology Inc. | Composition de dispersion polymere hydrophile contenant une silice colloidale, utile en tant qu'agent de retention de fines particules dans un systeme de fabrication de papier, et procede associe |
WO2000011052A1 (fr) * | 1998-08-24 | 2000-03-02 | Green Technology Inc. | Procede et composition de dispersion de polymeres hydrophiles contenant un floculant inorganique destine au traitement des eaux usees |
WO2000069938A1 (fr) * | 1999-05-12 | 2000-11-23 | Creavis Gesellschaft Für Technologie Und Innovation Mbh | Copolymeres microbicides |
US6225395B1 (en) | 1997-11-04 | 2001-05-01 | Elf Atochem, S.A. | Aqueous stable dispersions based on water-soluble polymers containing a cationic dispersant comprising hydrophobic units |
US6365052B1 (en) | 2000-03-21 | 2002-04-02 | Nalco Chemical Company | Very high molecular weight cationic dispersion polymers for dewatering animal farm wastewater |
FR2815635A1 (fr) * | 2000-10-23 | 2002-04-26 | Snf Sa | Dispersions aqueuses d'un polymere hydrosoluble, procede pour leurs preparations, et leurs applications |
US6398967B2 (en) | 2000-04-20 | 2002-06-04 | Nalco Chemical Company | Method of clarifying water using low molecular weight cationic dispersion polymers |
US6608124B1 (en) | 1996-10-03 | 2003-08-19 | Cytec Technology Corp. | Aqueous dispersions |
WO2003085232A1 (fr) | 2002-04-03 | 2003-10-16 | Nalco Energy Services, L.P. | Utilisation de polymeres de dispersion comme reducteurs de frottement dans des liquides de fracturation aqueux |
US6664326B1 (en) | 1996-10-03 | 2003-12-16 | Cytec Technology Corp. | Aqueous dispersions |
US6702946B1 (en) | 1996-10-03 | 2004-03-09 | Cytec Technology Corp. | Aqueous dispersions |
US7091273B2 (en) | 2002-05-07 | 2006-08-15 | Akzo Nobel N.V. | Process for preparing a polymer dispersion |
CN100386363C (zh) * | 2002-06-27 | 2008-05-07 | 湖北省化学研究所 | 高悬浮力水溶性防锈研磨液 |
US7641766B2 (en) | 2004-01-26 | 2010-01-05 | Nalco Company | Method of using aldehyde-functionalized polymers to enhance paper machine dewatering |
CN101016359B (zh) * | 2007-03-06 | 2010-06-02 | 山东东方华龙工贸集团有限公司 | 阳离子型聚丙烯酰胺水乳液的制备方法 |
WO2010093847A1 (fr) | 2009-02-13 | 2010-08-19 | Nalco Company | Composition antimicrobienne |
WO2011075650A2 (fr) | 2009-12-18 | 2011-06-23 | Nalco Company | Polymères fonctionnalisés par aldéhyde avec une stabilité accrue |
US8709207B2 (en) | 2010-11-02 | 2014-04-29 | Nalco Company | Method of using aldehyde-functionalized polymers to increase papermachine performance and enhance sizing |
US8840759B2 (en) | 2010-11-02 | 2014-09-23 | Ecolab Usa Inc. | Method of using aldehyde-functionalized polymers to increase papermachine performance and enhance sizing |
WO2014164380A1 (fr) | 2013-03-13 | 2014-10-09 | Nalco Company | Procédé d'utilisation de polymères à fonctionnalité aldéhyde pour augmenter les performances d'une machine à papier et améliorer l'encollage |
WO2016004228A1 (fr) | 2014-07-01 | 2016-01-07 | Ecolab Usa Inc. | Utilisation de polymères fluorescents dans des compositions de marquage permettant la détermination de diagnostic de réalisation de nettoyage |
WO2016032844A1 (fr) * | 2014-08-28 | 2016-03-03 | Dow Global Technologies Llc | Latex copolymères cationiques utiles en tant qu'additifs pour des applications de champ pétrolifère |
US9702086B2 (en) | 2014-10-06 | 2017-07-11 | Ecolab Usa Inc. | Method of increasing paper strength using an amine containing polymer composition |
EP3275844A1 (fr) | 2012-12-28 | 2018-01-31 | Ecolab USA Inc. | Monomères fluorescents pour la préparation de polymères de traitement marqués utiles dans des systèmes d'eau industriels |
US9920482B2 (en) | 2014-10-06 | 2018-03-20 | Ecolab Usa Inc. | Method of increasing paper strength |
US9951475B2 (en) | 2014-01-16 | 2018-04-24 | Ecolab Usa Inc. | Wet end chemicals for dry end strength in paper |
US10006170B2 (en) | 2015-08-06 | 2018-06-26 | Ecolab Usa Inc. | Aldehyde-functionalized polymers for paper strength and dewatering |
CN108431058A (zh) * | 2015-12-17 | 2018-08-21 | 巴斯夫欧洲公司 | 用于制备复合膜的低乳化剂含量的水性聚合物分散体 |
WO2018160818A1 (fr) | 2017-03-01 | 2018-09-07 | Ecolab Usa Inc. | Assainisseurs et désinfectants à risques d'inhalation réduits par l'intermédiaire de polymères de poids moléculaire élevé |
US10145067B2 (en) | 2007-09-12 | 2018-12-04 | Ecolab Usa Inc. | Method of improving dewatering efficiency, increasing sheet wet web strength, increasing sheet wet strength and enhancing filler retention in papermaking |
US10648133B2 (en) | 2016-05-13 | 2020-05-12 | Ecolab Usa Inc. | Tissue dust reduction |
WO2020247637A1 (fr) | 2019-06-07 | 2020-12-10 | Ecolab Usa Inc. | Polymères en dispersion cationique hydrophiles pour améliorer la qualité d'impression et la solidité à l'eau |
US11001748B2 (en) | 2008-11-10 | 2021-05-11 | Flotek Chemistry, Llc | Method of preparing and using a drag-reducing additive having a dispersion polymer |
US11560443B2 (en) | 2019-09-11 | 2023-01-24 | Buckman Laboratories International, Inc. | Grafted polyvinyl alcohol polymer, formulations containing the same, and creping methods |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0248519A2 (fr) * | 1986-05-30 | 1987-12-09 | Petrolite Corporation | Composition d'agent de floculation et sa méthode d'emploi |
EP0364175B1 (fr) * | 1988-10-14 | 1994-12-14 | Hymo Corporation | Procédé de préparation de polymères cationiques solubles dans l'eau |
-
1994
- 1994-12-06 AU AU80247/94A patent/AU8024794A/en not_active Abandoned
- 1994-12-08 KR KR1019940033220A patent/KR950018176A/ko not_active Application Discontinuation
- 1994-12-08 CA CA002137637A patent/CA2137637A1/fr not_active Abandoned
- 1994-12-09 JP JP6306180A patent/JPH07238121A/ja active Pending
- 1994-12-09 EP EP94119536A patent/EP0657478A3/fr not_active Withdrawn
- 1994-12-09 BR BR9404916A patent/BR9404916A/pt not_active Application Discontinuation
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0248519A2 (fr) * | 1986-05-30 | 1987-12-09 | Petrolite Corporation | Composition d'agent de floculation et sa méthode d'emploi |
EP0364175B1 (fr) * | 1988-10-14 | 1994-12-14 | Hymo Corporation | Procédé de préparation de polymères cationiques solubles dans l'eau |
Cited By (72)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AU710781B2 (en) * | 1996-07-09 | 1999-09-30 | Betzdearborn Inc. | Process for the preparation of aqueous dispersion polymers |
US5696194A (en) * | 1996-07-09 | 1997-12-09 | Betzdearborn Inc. | Process for the preparations of aqueous dispersion polymers |
US5614602A (en) * | 1996-07-09 | 1997-03-25 | Betzdearborn Inc. | Process for the preparation of aqueous dispersion polymers |
US5707533A (en) * | 1996-07-09 | 1998-01-13 | Betzdearborn Inc. | Process for the preparation of aqueous dispersion polymers |
WO1998001491A1 (fr) * | 1996-07-09 | 1998-01-15 | Betzdearborn Inc. | Procede pour la production de polymeres en dispersion aqueuse |
US5738794A (en) * | 1996-10-03 | 1998-04-14 | Cytec Technology Corp. | Cationic water-soluble polymer preciptation in salt solutions |
US5733462A (en) * | 1996-10-03 | 1998-03-31 | Cytec Technology Corp. | Cationic water-soluble polymer precipitation in salt solutions |
US5792366A (en) * | 1996-10-03 | 1998-08-11 | Cytec Technology Corp. | Aqueous dispersions |
US5843320A (en) * | 1996-10-03 | 1998-12-01 | Cytec Technology Corp. | Aqueous dispersions |
US5696228A (en) * | 1996-10-03 | 1997-12-09 | Cytec Technology Corp. | Process for producing substantially dry polymer particles from aqueous dispersions |
US6702946B1 (en) | 1996-10-03 | 2004-03-09 | Cytec Technology Corp. | Aqueous dispersions |
US5919854A (en) * | 1996-10-03 | 1999-07-06 | Cytec Technology Corp. | Process for preparing aqueous dispersions |
US6608124B1 (en) | 1996-10-03 | 2003-08-19 | Cytec Technology Corp. | Aqueous dispersions |
US6013708A (en) * | 1996-10-03 | 2000-01-11 | Cytec Technology Corp. | Cationic water-soluble polymer precipitation in salt solutions |
US6664326B1 (en) | 1996-10-03 | 2003-12-16 | Cytec Technology Corp. | Aqueous dispersions |
US6020422A (en) * | 1996-11-15 | 2000-02-01 | Betzdearborn Inc. | Aqueous dispersion polymers |
EP0915107A1 (fr) * | 1997-11-04 | 1999-05-12 | Elf Atochem S.A. | Dispersions aqueuses salines de polymères hydrosolubles contenant un dispersant amphiphile à base de polymère cationique ayant des motifs hydrophobes |
FR2770527A1 (fr) * | 1997-11-04 | 1999-05-07 | Atochem Elf Sa | Dispersions aqueuses salines de polymeres hydrosolubles contenant un dispersant amphiphile a base de polymere cationique ayant des motifs hydrophobes |
US6221957B1 (en) | 1997-11-04 | 2001-04-24 | Elf Atochem S.A. | Aqueous saline dispersions of water-soluble polymers containing an amphiphilic dispersant based on a cationic polymer containing hydrophobic units |
US6225395B1 (en) | 1997-11-04 | 2001-05-01 | Elf Atochem, S.A. | Aqueous stable dispersions based on water-soluble polymers containing a cationic dispersant comprising hydrophobic units |
KR100294785B1 (ko) * | 1997-11-04 | 2001-07-12 | 베아트리체 델로스탈 | 소수성단위함유양이온성고분자기제의양친매성분산제를함유하는수용성고분자의수성함염분산액 |
US6531531B1 (en) | 1998-08-24 | 2003-03-11 | Green Technology Inc. | Method and composition of a hydrophilic polymer dispersion containing an inorganic flocculant to be used for the treatment of waste water |
WO2000011052A1 (fr) * | 1998-08-24 | 2000-03-02 | Green Technology Inc. | Procede et composition de dispersion de polymeres hydrophiles contenant un floculant inorganique destine au traitement des eaux usees |
US6630530B1 (en) * | 1998-08-24 | 2003-10-07 | Green Technology Inc. | Method and composition of a hydrophilic polymer dispersion containing a colloidal silica to be used for the retention aids of fine particles in papermaking system |
WO2000011053A1 (fr) * | 1998-08-24 | 2000-03-02 | Green Technology Inc. | Composition de dispersion polymere hydrophile contenant une silice colloidale, utile en tant qu'agent de retention de fines particules dans un systeme de fabrication de papier, et procede associe |
WO2000069938A1 (fr) * | 1999-05-12 | 2000-11-23 | Creavis Gesellschaft Für Technologie Und Innovation Mbh | Copolymeres microbicides |
US6365052B1 (en) | 2000-03-21 | 2002-04-02 | Nalco Chemical Company | Very high molecular weight cationic dispersion polymers for dewatering animal farm wastewater |
US6398967B2 (en) | 2000-04-20 | 2002-06-04 | Nalco Chemical Company | Method of clarifying water using low molecular weight cationic dispersion polymers |
US6517677B1 (en) | 2000-04-20 | 2003-02-11 | Ondeo Nalco Company | Method of improving retention and drainage in a papermaking process using low molecular weight cationic dispersion polymers |
FR2815635A1 (fr) * | 2000-10-23 | 2002-04-26 | Snf Sa | Dispersions aqueuses d'un polymere hydrosoluble, procede pour leurs preparations, et leurs applications |
WO2002034796A1 (fr) * | 2000-10-23 | 2002-05-02 | Snf S.A. | Dispersions aqueuses d'un polymere hydrosoluble, procede pour leurs preparations, et leurs applications |
WO2003085232A1 (fr) | 2002-04-03 | 2003-10-16 | Nalco Energy Services, L.P. | Utilisation de polymeres de dispersion comme reducteurs de frottement dans des liquides de fracturation aqueux |
US7091273B2 (en) | 2002-05-07 | 2006-08-15 | Akzo Nobel N.V. | Process for preparing a polymer dispersion |
US7220339B2 (en) | 2002-05-07 | 2007-05-22 | Akzo Nobel N.V. | Process for preparing a polymer dispersion |
CN100386363C (zh) * | 2002-06-27 | 2008-05-07 | 湖北省化学研究所 | 高悬浮力水溶性防锈研磨液 |
US7641766B2 (en) | 2004-01-26 | 2010-01-05 | Nalco Company | Method of using aldehyde-functionalized polymers to enhance paper machine dewatering |
USRE44936E1 (en) * | 2004-01-26 | 2014-06-10 | Nalco Company | Aldehyde-functionalized polymers |
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Also Published As
Publication number | Publication date |
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EP0657478A3 (fr) | 1995-07-26 |
JPH07238121A (ja) | 1995-09-12 |
CA2137637A1 (fr) | 1995-06-10 |
AU8024794A (en) | 1995-06-15 |
BR9404916A (pt) | 1995-08-08 |
KR950018176A (ko) | 1995-07-22 |
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